[go: up one dir, main page]

US1861415A - Treatment of electrodes - Google Patents

Treatment of electrodes Download PDF

Info

Publication number
US1861415A
US1861415A US540808A US54080831A US1861415A US 1861415 A US1861415 A US 1861415A US 540808 A US540808 A US 540808A US 54080831 A US54080831 A US 54080831A US 1861415 A US1861415 A US 1861415A
Authority
US
United States
Prior art keywords
electrode
oil
electrodes
carbon
impregnated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US540808A
Inventor
Ralph M Hunter
Leroy C Stewart
Howard E Houser
Pree Lee De
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dow Chemical Co filed Critical Dow Chemical Co
Priority to US540808A priority Critical patent/US1861415A/en
Application granted granted Critical
Publication of US1861415A publication Critical patent/US1861415A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/009After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/45Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
    • C04B41/52Multiple coating or impregnating multiple coating or impregnating with the same composition or with compositions only differing in the concentration of the constituents, is classified as single coating or impregnation
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/80After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only ceramics
    • C04B41/81Coating or impregnation
    • C04B41/89Coating or impregnation for obtaining at least two superposed coatings having different compositions
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/042Electrodes formed of a single material
    • C25B11/043Carbon, e.g. diamond or graphene
    • C25B11/044Impregnation of carbon

Definitions

  • This invention concerns an improved method for impregnating porous articles of carbon, graphite, graphitized carbon, or the like, for the purpose of prolongingthe useful' life or other characteristics thereof; and is particularly applicable to the preparation of such articles to resist chemical attack, such as occurs when the same are used as electrodes in the electrolysis of alkali metal halides or for parts of electrolytic cells, etc: where sub ject to oxidizing action.
  • a carbon or graphite electrode when used in a process for electrolyzing alkali metal chloride solutions, tends to absorb the salt solution, chlorine and oxygen are liberated Within the voids of the electrode and as a result it becomes oxidized throughout and disintegrates.
  • the present invention involves a further modification of the above described processes for treatment of carbon electrodes, but is an improvement over all known methods in that the product obtained by the herein described process consists of a carbon and/or graphite electrode which has not only been impregnated with Chinawood oil but which has been further treated in such a manner as to both chlorinate and polymerize (or coagulate) the so usedoil within the voids of the electrode.
  • a carbon and/or graphite electrode is impregnated with Chinawood oil, then the so used oil simultaneously chlorinated and polymerized within said electrode by means of a chloride ion containing solution of a strong mineral acid and a olymerizing salt.
  • Free chlorine is preferably. but not necessarily, present in the above mentioned mineral acid solution during treatment of the impregnated electrode therewith.
  • Example 1 A graphitized carbon plate was placed in a suitable air tight container and the latter evacuated to an absolute pressure of approximately 110 millimeters. Chinawood oil was then admitted to the container and the pressure thereon brought to and maintained at 125 pounds gauge during a period of 5 hours. The-oil was then drained from the container and steam admitted thereto, in order to facilitate draining of excess oil adhering to the plate. (The oil content of a plate, at this point, is generally found to be approximately 9 to 12 per cent of the original weight of the latter, which means that I approximately 5080 per cent of the original voids in the plate are filled with oil).
  • the container containing the graphite plate was again evacuated to an absolute pressure of approximatelyllO millimeters and maintained at that pressure for about 2 minutes. then air admitted.
  • the plate was removed from its container and plunged, while hot. into a solution of ferric chloride in hydrochloric acid where it was permitted to cool to room temperature, then removed and dried. The plate was then ready for use as an electrode in the previously mentioned electrolytic process.
  • Example 2 A graphitized carbon plate was treated in a way similar to that described in Example 1, except that chlorine was passed through the solution of ferric chloride in hydrochloric acid during the time the impregnated plate was immersed and cooling therein. It was found, upon analysis ofvarious' cuts from cross-sections both of this plate and of the plate described in Example 1, that in the present example the polymerized oil was chlorinated at a greater depth from the surface of the electrode and more uniformly than it was in the product obtained according to the method described in Example 1.
  • Electrodes prepared according to our method. have beenlfound to be impervious to penetration by brine and to be very resistant to further action by the chlorine liberated during the aforementioned electrolytic process. Tests made indicate that they have a longer active life than do such electrodes treated by any previously described process.
  • carbon and/or raphite shall be used to characterize an e ectrode or article composed chiefly of carbon, graphite, or graphitized carbon.
  • a method of treating a carbon and/0r graphite electrode the steps which consist in mpregnating said electrode with Chinawood oil, heating the impregnated electrode with steam, then cooling said electrode in a hydrochloric acid solution containing at least Zine of the following group of salts :ferric graphite electrode, the steps which consist in treating such an electrode,-impregnated with Chinawood oil, with steam, then cooling said electrode in a hydrochloric acid solution containing free chlorine and also containing at least one of the following group of salts ferric chloride, ferric sulphate, ferricnitrate, a gimony pentachloride, titanium tetrachlor1 e.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Metallurgy (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Ceramic Products (AREA)

Description

A Patented May 31, 1 932 UNITED STATES PATENT-L OFFICE 'f RALBH M. HUNTER, LEROY C. STEWART, HOWARD E. HOUSER, AND LEE DE PBEE, OI MIDLAND, MICHIGAN, ASSIGNORS TO THE DOW CHEMICAL COMPANY, OI MIDLAND, MICHIGAN, A CORPORATION ,OF MICHIGAN I N0 Drawing.
This invention concerns an improved method for impregnating porous articles of carbon, graphite, graphitized carbon, or the like, for the purpose of prolongingthe useful' life or other characteristics thereof; and is particularly applicable to the preparation of such articles to resist chemical attack, such as occurs when the same are used as electrodes in the electrolysis of alkali metal halides or for parts of electrolytic cells, etc: where sub ject to oxidizing action.
A carbon or graphite electrode, when used in a process for electrolyzing alkali metal chloride solutions, tends to absorb the salt solution, chlorine and oxygen are liberated Within the voids of the electrode and as a result it becomes oxidized throughout and disintegrates. In order to prevent such action, it is general practice to impregnate the electrodes with oils, waxes or the like prior to using them in the aforementioned process. Such treatment increases theefi'iciency of the electrolytic process and materially lengthens the life of the-electrodes themselves. While paraflin oil and waxes are generally used for impregnating electrodes, it has been found that better results are obtained when Chinawood oil and similar drying oils are substituted therefor.
Although treatment of electrodes, in the manner described above,.decreases the diffusion of brine through the same and in general improves their quality, certain disadvantages result from such practice." During use of the so treated electrodes in the process for electrolyzing alkali metal chlorides, for instance, the oil with which they are impregn ated becomes partially chlorinated and tends to swell, with the result that the electrodes sweat oil and at the same time crumble or wear away. The oil or wax so lib erated from the electrodes 'proves further disadvantageous in that it tends to foul and obstruct the cell diaphragm, thereby interfering with the conduct ofthe'process as a whole. However. after an electrode impregnated in the described manner has been larges, 1y worn away, the portion thereof'remaining is found to be hard; it no longer sweats oil; it is impervious to bririe; and further TREATMENT or ELECTRODES Application filed May 28, 1931. Serial no. smsos.
oxidation and distintegration of said remnant electrode proceeds with extreme slowness. This change in character of the electrode is believed to result from the oil remaining therein having become as completeso thereafter absent. It is therefore desirable 00 I I to change the character of impregnated elec-:
trodes to that last described before using the same.
An improved process for impregnatingcarbon electrodes, described by O. A. Laubi 05 w in United States Patent 1,779,242, consists in impregnating such electrodes with ch10: rinated hydrocarbons before using the same in electrolytic cells. By such treatment, further chlorination of the hydrocarbon oils (0 in a co-pending application of R. M. Hunter 15 and L. E. Ward, Serial No. 461,632, filed June 16, 1930. Briefly, their process consists in first impregnating carbon or graphite electrodes with a drying oil, e. g. Chinawood oil, then subjecting the impregnated'electrodes to the action of chlorine over a con,- siderable period of time. Although an electrode treated in such a manner often has an active life which exceeds that of one impreg-i nated with Chinawood oil but not prechlorinated by as much as 50 per cent, the process is still disadvantageous in that the chlorination step proceeds slowly, generally requiring aperiod of several weeksor even months for appreciable chlorination of the impregnating oil to be effected. Furthermore, chlorination occurs most readily at the surface of the electrode and is liable to be non-uniform in depth of penetration- Therefore, electrodes treated in such a manner are not consistent in quality. In another co-pending ap 1ication of R. M. Hunter and L. E; Ward, erial No. 513.049, filed February 2, 1931, and entitled Process for treating electrodes, a process is described whereby carbon or graphite electrodes are impregnated with a prechlorinated drying oil such as Chinawood oil. Such treatment has been found to pro duce a product, uniform in quality, and superior in durability'to electrodes prepared by the other mentioned processes.
' The present invention involves a further modification of the above described processes for treatment of carbon electrodes, but is an improvement over all known methods in that the product obtained by the herein described process consists of a carbon and/or graphite electrode which has not only been impregnated with Chinawood oil but which has been further treated in such a manner as to both chlorinate and polymerize (or coagulate) the so usedoil within the voids of the electrode. We havefound that a carbon and/or graphite electrode, impregnated with Chinawood oil, when treated with a chloride ion containing solution of a strong mineral acid and at least one of the followin group of salts :-.ferric chloride, ferric sul ate, ferric nitrate, antimony pentachloride and titanium tetrachloride, is acted upon in such a manner that the oil therein is both polymerized and partially chlorinated, the result being that the electrode is rendered impervious to penetration by brine and very resistant to further action by chlorine. The present invention, then, consists of a process, and of the product from said process, hereinafter fully described and articularly pointedout in the claims, where,-
y a carbon and/or graphite electrode is impregnated with Chinawood oil, then the so used oil simultaneously chlorinated and polymerized within said electrode by means of a chloride ion containing solution of a strong mineral acid and a olymerizing salt. Free chlorine is preferably. but not necessarily, present in the above mentioned mineral acid solution during treatment of the impregnated electrode therewith. V
Preliminary to the treatment of electrodes in the manner hereinafter described, tests were made to determine the effect of hydrochloric acid solutions of various salts upon Chinawood oil. Into a test tube were placed 10 cubic centimeters of a solution consisting of 50 per cent Chinawood oil and 50 per cent kerosene, by weight. To this solution were added 0.1 gram of ferric chloride, 0.5 gram of concentrated (37 per cent) hydrochloric acid and 0.5 gram of water. The mixture was thoroughly agitated, then permitted to stand at room temperature. In approximately 20 minutes the Chinawood oil was polymerized toa solid mass. The liquid remaining after such treatment was found to contain ferrous chloride, and analysis of the polymerized product proved it to have been partially chlorinated. By means of similar tests it was found that a similar chlorinated and polymerized product could be obtained by using ferric nitrate, ferric sulfate, or antimony pentachloride instead of the aforementioned ferric chloride. It was also found that titanium tetrachloride would produce the above described polymer, if used in a concentrated form.
' Several of the various ways of applying the principle of our invention are described in the following examples. It is to be understood, however, that such examples are purely illustrative and are not to be construed as a limitation on the invention.
Example 1 A graphitized carbon plate was placed in a suitable air tight container and the latter evacuated to an absolute pressure of approximately 110 millimeters. Chinawood oil was then admitted to the container and the pressure thereon brought to and maintained at 125 pounds gauge during a period of 5 hours. The-oil was then drained from the container and steam admitted thereto, in order to facilitate draining of excess oil adhering to the plate. (The oil content of a plate, at this point, is generally found to be approximately 9 to 12 per cent of the original weight of the latter, which means that I approximately 5080 per cent of the original voids in the plate are filled with oil). After treatment .with steam, the container containing the graphite plate was again evacuated to an absolute pressure of approximatelyllO millimeters and maintained at that pressure for about 2 minutes. then air admitted. The plate was removed from its container and plunged, while hot. into a solution of ferric chloride in hydrochloric acid where it was permitted to cool to room temperature, then removed and dried. The plate was then ready for use as an electrode in the previously mentioned electrolytic process.
Example 2 A graphitized carbon plate was treated in a way similar to that described in Example 1, except that chlorine was passed through the solution of ferric chloride in hydrochloric acid during the time the impregnated plate was immersed and cooling therein. It was found, upon analysis ofvarious' cuts from cross-sections both of this plate and of the plate described in Example 1, that in the present example the polymerized oil was chlorinated at a greater depth from the surface of the electrode and more uniformly than it was in the product obtained according to the method described in Example 1.
-Electrodes, prepared according to our method. have beenlfound to be impervious to penetration by brine and to be very resistant to further action by the chlorine liberated during the aforementioned electrolytic process. Tests made indicate that they have a longer active life than do such electrodes treated by any previously described process.
In the claims it shallbe' understood that the term carbon and/or raphite shall be used to characterize an e ectrode or article composed chiefly of carbon, graphite, or graphitized carbon.
Other forms of applying'theprinciple of our invention may be employed instead of the ones here explained, change being made in the method or composition, provided the steps or 5 ingredients stated by any of the following claims or the equivalent of such stated steps or ingredients be employed.
We therefore particularly point out and distinctly claim as our invention 1. In a method of treating a carbon and/or graphite article, the steps which consist in impregnating said article with Chinawood oil and then simultaneously chlorinating and polymerizing said oil by means of a chloride ion containing solution of a strong mineral acid and a polymerizing salt.
2. In a method of treating a carbon and/or graphite electrodeAshe steps which consist in impregnating said electrode with Chinawood oil, then further subjecting the thus impregnated electrode to the action of a hydrochloric acid solution containing at least one of the following group of salts :-ferric chloride,'ferric sulphate, ferric nitrate, anti- -mony pentachloride, titanium tetrachloride.
3. In a method of treating a carbon and/or graphite electrode, the steps which consist in impregnating said electrode with Chinawood oil, heating the impregnated electrode with steam,'then cooling. said electrode in a hydrochloric acid solution containing free chlorine and also containing at least one of I the following group of salts :f'erric chloride, ferric sulphate, ferric nitrate, antimony pentachloride, titanium tetrachloride. 4. In a method of treating a carbon and/0r graphite electrode, the steps which consist in mpregnating said electrode with Chinawood oil, heating the impregnated electrode with steam, then cooling said electrode in a hydrochloric acid solution containing at least Zine of the following group of salts :ferric graphite electrode, the steps which consist in treating such an electrode,-impregnated with Chinawood oil, with steam, then cooling said electrode in a hydrochloric acid solution containing free chlorine and also containing at least one of the following group of salts ferric chloride, ferric sulphate, ferricnitrate, a gimony pentachloride, titanium tetrachlor1 e. i
8. In a method of treating a carbon and/0r graphite electrode, the steps which consist in treating such an'electrode, impregnated with Chinawood oil, with steam, then cooling said electrode in a hydrochloric acid solution containing at least one of the following group of and/or graphite electrode, the steps which consist in impregnating said electrode with Chinawood oil, then treating the so impregnated electrode with steam, and finally coo ing the electrode in a hydrochloric acid solution containing ferric chloride.
11. As a product of manufacture, a carbon and/or graphite article impregnated with a polymerized form of Chinawood oil which is at least in part chlorinated.
12. As a product of manufacture, a carbon and/or graphite electrode impregnated with a polymerized form of Chinawood oil which is at east in part chlorinated.
Signed by us this 23rd day of May 1931. RALPH M. HUNTER.
LEROY C. STEWART. HOWARD E. HOUSER. LEE DE FREE, I
chloride, ferric sul hate, ferric nitrate, antimony pentachlori e, titanium tetrachloride.
5. In a method of treating a carbon and/or graphite electrode, wood oil, the step which consists in simultaneously chlorinating and polymerizing said oil by means of a chloride ion containing soluton of a strong mineral acid and a polymerizing salt.
reg'nated. with China- I I 6. In a meth 'od of treating a carbon and/or' graphite electrodedhe step which consists i3 ate Sub ecting such an electrode; impre with chinawood oilfto the action a hydrochloric acid solution containing at leg'st one of the'following group of salts :e-ferric chloride, ferric sulphate, ferric nitrate, antimony pentachloride, titanium tetrachloride.
7. a method of treating a carbon and/or
US540808A 1931-05-28 1931-05-28 Treatment of electrodes Expired - Lifetime US1861415A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US540808A US1861415A (en) 1931-05-28 1931-05-28 Treatment of electrodes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US540808A US1861415A (en) 1931-05-28 1931-05-28 Treatment of electrodes

Publications (1)

Publication Number Publication Date
US1861415A true US1861415A (en) 1932-05-31

Family

ID=24157019

Family Applications (1)

Application Number Title Priority Date Filing Date
US540808A Expired - Lifetime US1861415A (en) 1931-05-28 1931-05-28 Treatment of electrodes

Country Status (1)

Country Link
US (1) US1861415A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2418420A (en) * 1943-02-08 1947-04-01 Westinghouse Electric Corp Process for impregnating carbon brushes
US2433212A (en) * 1942-10-09 1947-12-23 Ici Ltd Electrode for use in electrolytic cells
US2500209A (en) * 1946-07-11 1950-03-14 Great Lakes Carbon Corp Production of shaped carbon articles
US2820728A (en) * 1955-06-21 1958-01-21 Diamond Alkali Co Method of treating carbon electrodes with polymerizable oil
US2920004A (en) * 1958-02-20 1960-01-05 Columbia Southern Chem Corp Method of treating drying oil impregnated graphite electrode
US3057794A (en) * 1961-10-10 1962-10-09 Pittsburgh Plate Glass Co Electrolytic cell diaphragm

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2433212A (en) * 1942-10-09 1947-12-23 Ici Ltd Electrode for use in electrolytic cells
US2418420A (en) * 1943-02-08 1947-04-01 Westinghouse Electric Corp Process for impregnating carbon brushes
US2500209A (en) * 1946-07-11 1950-03-14 Great Lakes Carbon Corp Production of shaped carbon articles
US2820728A (en) * 1955-06-21 1958-01-21 Diamond Alkali Co Method of treating carbon electrodes with polymerizable oil
US2920004A (en) * 1958-02-20 1960-01-05 Columbia Southern Chem Corp Method of treating drying oil impregnated graphite electrode
US3057794A (en) * 1961-10-10 1962-10-09 Pittsburgh Plate Glass Co Electrolytic cell diaphragm

Similar Documents

Publication Publication Date Title
SU505332A3 (en) The method of obtaining a porous diaphragm for electrolysis
US2129289A (en) Manufacture of new fluorine compounds
US1861415A (en) Treatment of electrodes
US3580824A (en) Impregnated graphite
US3057794A (en) Electrolytic cell diaphragm
DE1471546B2 (en) WITH INORGANIC CHEMICALLY RESISTANT HYDROPHOBIC OIL REPELLENT AND LUBRICANT POLYCARBON FLUORIDE OF FORMULA CF DEEP N COATED CARBON PARTS
US2820728A (en) Method of treating carbon electrodes with polymerizable oil
US2067738A (en) Method of treating carbonaceous electrode-elements
Lowson Aluminium corrosion studies. IV. Pitting corrosion
US1946153A (en) Protecting aluminum from corrosion
US1927661A (en) Process for treating electrodes
US2902386A (en) Carbon electrode oil impregnation method
US3046216A (en) Impregnated carbonaceous electrode and method of making the same
US1996643A (en) Improved electrode and method of making same
US2813825A (en) Method of producing perchlorates
US1547539A (en) Process for increasing the life of graphite or carbon electrodes
US1868206A (en) Treating electrodes
US2366712A (en) Method of anodically polishing stainless steel
US2433212A (en) Electrode for use in electrolytic cells
US2870074A (en) Electrolysis of alkali metal chloride brine
US2293266A (en) Chemical apparatus
US1779242A (en) Process of impregnating carbon electrodes
US3345283A (en) Process for producing a graphite anode
US1598018A (en) Process of electrolytic decomposition of chlorides
Jakšić The effect of pH on graphite wear in a chlorate cell process